Coperion GmbH

Stuttgart Muhlhausen, Germany

Coperion GmbH

Stuttgart Muhlhausen, Germany
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Browse 162 tables and 52 figures, 13 Company profiles spread across 181 pages available at The global continuous manufacturing market is expected to reach USD 650.4 million by 2022 from USD 348.5 million in 2017, at a CAGR of 13.3%. The market is segmented on the basis of product, application, end user, and geography. The product segment includes integrated systems, semi-continuous systems, and controls. The integrated systems segment is expected to account for the largest share of the continuous manufacturing market in 2017. The integrated systems enable end-to-end manufacturing to convert raw materials into final products. In addition, these systems save substantial cost and time by integrating various pharmaceutical processes in a single system. By application, the end product manufacturing segment is estimated to account for the largest share of the market, in 2017. FDA approval for certain drugs manufactured by the continuous process is the primary factor driving the growth of this segment. On the basis of end user, the full-scale manufacturing companies are expected to hold the highest share of the market, in 2017. The large share of this segment can primarily be attributed to the increasing adoption of continuous technologies by pharmaceutical manufacturing companies and CMOs to address the challenges related to product quality, drug supply, and operational costs. The geographic segments in this report include North America, Europe, Asia-Pacific, and RoW. Of these, the North American segment is expected to account for the largest share of the market in 2017. This large share can primarily be attributed to the support from regulatory bodies, initiation by leading pharmaceutical companies, and the need for pharmaceutical manufacturers to reduce rising operational costs and eliminate issues related to the inconsistent quality of pharmaceutical products produced through batch manufacturing. Product launch was the dominant strategy adopted by key industry participants to increase their market share and cater to unmet needs. Major players include GEA Group AG (Germany), Thermo Fisher Scientific Inc. (U.S.), Bosch Packaging Technology (Germany), Coperion GmbH (Germany), and Glatt GmbH (Germany). Other players include KORSCH AG (Germany), Munson Machinery Company, Inc. (U.S.), L.B. Bohle Maschinen + Verfahren Gmbh (Germany), Gebruder Lodige Maschinenbau GmbH (Germany), Baker Perkins Ltd. (U.K.), Scott Equipment Company (U.S.), and Sturtevant, Inc. (U.S.). Order a copy of Continuous Manufacturing Market By Product (Integrated system, Semi-continuous (Granulator, Coater, Blender), Control), Application (API, End Product (Solid Dosage)), End User (R&D Department (CRO), Pharmaceutical Companies, CMO) - Global Forecast to 2022 Research Report at Nuclear Medicine/Radiopharmaceuticals Market by Type (Diagnostic (SPECT - Technetium, PET - F-18), Therapeutic (Beta Emitters - I-131, Alpha Emitters, Brachytherapy - Y-90) & by Application (Oncology, Thyroid, Cardiology) - Global Forecasts to 2021. Explore more reports on Pharmaceuticals market Research at ReportsnReports.com is an online market research reports library of 500,000+ in-depth studies of over 5000 micro markets. Not limited to any one industry, ReportsnReports.com offers research studies on agriculture, energy and power, chemicals, environment, medical devices, healthcare, food and beverages, water, advanced materials and much more.


— In this report, the global Continuous Manufacturing market is valued at USD XX million in 2016 and is expected to reach USD XX million by the end of 2022, growing at a CAGR of XX% between 2016 and 2022. Geographically, this report is segmented into several key Regions, with production, consumption, revenue (million USD), market share and growth rate of Continuous Manufacturing in these regions, from 2012 to 2022 (forecast), covering United States EU China Japan South Korea Taiwan For more information or any query mail at sales@wiseguyreports.com Global Continuous Manufacturing market competition by top manufacturers, with production, price, revenue (value) and market share for each manufacturer; the top players including GEA Group Thermo Fisher Scientific Bosch Packaging Coperion GmbH Glatt GmbH Korsch AG Munson Machinery Company, Inc. L.B. Bohle Maschinen + Verfahren GmbH Bosch Packaging Technology Gebrüder Ldige Maschinenbau GmbH Baker Perkins Ltd. Scott Equipment Company Sturtevant, Inc. On the basis of product, this report displays the production, revenue, price, market share and growth rate of each type, primarily split into Integrated system Semi-continuous On the basis on the end users/applications, this report focuses on the status and outlook for major applications/end users, consumption (sales), market share and growth rate of Continuous Manufacturing for each application, including End Product Manufacturing Solid Dosage Liquid Dosage API Manufacturing Global Continuous Manufacturing Market Research Report 2017 1 Continuous Manufacturing Market Overview 1.1 Product Overview and Scope of Continuous Manufacturing 1.2 Continuous Manufacturing Segment by Type (Product Category) 1.2.1 Global Continuous Manufacturing Production and CAGR (%) Comparison by Type (Product Category) (2012-2022) 1.2.2 Global Continuous Manufacturing Production Market Share by Type (Product Category) in 2016 1.2.3 Integrated system 1.2.4 Semi-continuous 1.3 Global Continuous Manufacturing Segment by Application 1.3.1 Continuous Manufacturing Consumption (Sales) Comparison by Application (2012-2022) 1.3.2 End Product Manufacturing 1.3.3 Solid Dosage 1.3.4 Liquid Dosage 1.3.5 API Manufacturing 1.4 Global Continuous Manufacturing Market by Region (2012-2022) 1.4.1 Global Continuous Manufacturing Market Size (Value) and CAGR (%) Comparison by Region (2012-2022) 1.4.2 United States Status and Prospect (2012-2022) 1.4.3 EU Status and Prospect (2012-2022) 1.4.4 China Status and Prospect (2012-2022) 1.4.5 Japan Status and Prospect (2012-2022) 1.4.6 South Korea Status and Prospect (2012-2022) 1.4.7 Taiwan Status and Prospect (2012-2022) 1.5 Global Market Size (Value) of Continuous Manufacturing (2012-2022) 1.5.1 Global Continuous Manufacturing Revenue Status and Outlook (2012-2022) 1.5.2 Global Continuous Manufacturing Capacity, Production Status and Outlook (2012-2022) 2 Global Continuous Manufacturing Market Competition by Manufacturers 2.1 Global Continuous Manufacturing Capacity, Production and Share by Manufacturers (2012-2017) 2.1.1 Global Continuous Manufacturing Capacity and Share by Manufacturers (2012-2017) 2.1.2 Global Continuous Manufacturing Production and Share by Manufacturers (2012-2017) 2.2 Global Continuous Manufacturing Revenue and Share by Manufacturers (2012-2017) 2.3 Global Continuous Manufacturing Average Price by Manufacturers (2012-2017) 2.4 Manufacturers Continuous Manufacturing Manufacturing Base Distribution, Sales Area and Product Type 2.5 Continuous Manufacturing Market Competitive Situation and Trends 2.5.1 Continuous Manufacturing Market Concentration Rate 2.5.2 Continuous Manufacturing Market Share of Top 3 and Top 5 Manufacturers 2.5.3 Mergers & Acquisitions, Expansion 7 Global Continuous Manufacturing Manufacturers Profiles/Analysis 7.1 GEA Group 7.1.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.1.2 Continuous Manufacturing Product Category, Application and Specification 7.1.2.1 Product A 7.1.2.2 Product B 7.1.3 GEA Group Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.1.4 Main Business/Business Overview 7.2 Thermo Fisher Scientific 7.2.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.2.2 Continuous Manufacturing Product Category, Application and Specification 7.2.2.1 Product A 7.2.2.2 Product B 7.2.3 Thermo Fisher Scientific Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.2.4 Main Business/Business Overview 7.3 Bosch Packaging 7.3.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.3.2 Continuous Manufacturing Product Category, Application and Specification 7.3.2.1 Product A 7.3.2.2 Product B 7.3.3 Bosch Packaging Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.3.4 Main Business/Business Overview 7.4 Coperion GmbH 7.4.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.4.2 Continuous Manufacturing Product Category, Application and Specification 7.4.2.1 Product A 7.4.2.2 Product B 7.4.3 Coperion GmbH Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.4.4 Main Business/Business Overview 7.5 Glatt GmbH 7.5.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.5.2 Continuous Manufacturing Product Category, Application and Specification 7.5.2.1 Product A 7.5.2.2 Product B 7.5.3 Glatt GmbH Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.5.4 Main Business/Business Overview 7.6 Korsch AG 7.6.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.6.2 Continuous Manufacturing Product Category, Application and Specification 7.6.2.1 Product A 7.6.2.2 Product B 7.6.3 Korsch AG Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.6.4 Main Business/Business Overview 7.7 Munson Machinery Company, Inc. 7.7.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.7.2 Continuous Manufacturing Product Category, Application and Specification 7.7.2.1 Product A 7.7.2.2 Product B 7.7.3 Munson Machinery Company, Inc. Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.7.4 Main Business/Business Overview 7.8 L.B. Bohle Maschinen + Verfahren GmbH 7.8.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.8.2 Continuous Manufacturing Product Category, Application and Specification 7.8.2.1 Product A 7.8.2.2 Product B 7.8.3 L.B. Bohle Maschinen + Verfahren GmbH Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.8.4 Main Business/Business Overview 7.9 Bosch Packaging Technology 7.9.1 Company Basic Information, Manufacturing Base, Sales Area and Its Competitors 7.9.2 Continuous Manufacturing Product Category, Application and Specification 7.9.2.1 Product A 7.9.2.2 Product B 7.9.3 Bosch Packaging Technology Continuous Manufacturing Capacity, Production, Revenue, Price and Gross Margin (2012-2017) 7.9.4 Main Business/Business Overview For more information or any query mail at sales@wiseguyreports.com ABOUT US: Wise Guy Reports is part of the Wise Guy Consultants Pvt. Ltd. and offers premium progressive statistical surveying, market research reports, analysis & forecast data for industries and governments around the globe. Wise Guy Reports features an exhaustive list of market research reports from hundreds of publishers worldwide. We boast a database spanning virtually every market category and an even more comprehensive collection of rmaket research reports under these categories and sub-categories. For more information, please visit https://www.wiseguyreports.com


Patent
Coperion GmbH | Date: 2012-02-06

A device for producing granules has a water-cooled granulating mechanism for producing plastics material granules. A discharge line arranged downstream of the granulating mechanism discharges a starting mixture flow and a granule heat exchanger arranged downstream of the discharge line controls the temperature of the mixture containing the plastics material granules and cooling water using parallel fluid passages. The granule heat exchanger has an inlet and an outlet for a transmission heat exchanger medium. A drying mechanism arranged downstream of the granule heat exchanger dries the plastics material granules. The device also may have an energy recovery mechanism arranged downstream of the discharge line for recovering energy from a recovery cooling water flow, containing at least a part of the cooling water of the starting mixture flow. The device uses waste heat, transmitted to the cooling water to increase the performance of the device and improve the energy efficiency thereof.


In a processing plant for producing plastics material granulate, the start-up takes place in such a way that a screw machine is firstly driven by means of a drive device and then plastics material to be processed is fed by means of a metering device into the screw machine. At least one conveying position of the plastics material in the screw machine is determined by means of a control device by evaluating at least one measuring signal. Depending on the conveying position determined, a granulating device is activated and put into operation. The method according to the invention allows a direct start-up of the processing plant without the use of a start-up valve. This ensures an easy and safe start-up of the processing plant.


A loading system for loading bulk material from a bulk material production plant onto a ship has at least one stationary intermediate storage container for receiving the bulk material from the bulk material production plant. A first loading conveying device is used to convey the bulk material from the bulk material production plant into the intermediate storage container. A second loading conveying device is used to convey the bulk material from the intermediate storage container into the ship. An unloading system for loading bulk material from a ship onto transporters has a stationary intermediate storage container for receiving the bulk material from the ship. Two unloading conveying devices are used to convey the bulk material, from the ship into the intermediate storage container and, from the intermediate storage container into the transporters.


A device, to homogenise plastics material melts, has a homogenising element with a plurality of flow channels, which differ with respect to at least one feature from the group length, cross sectional area and cross sectional shape. When flowing through the homogenising element, the plastics material melt is divided into a plurality of part streams, which, in each case, flow through an associated flow channel. When leaving the respective flow channel the part streams have different flow speeds so the plastics material melt is expanded and sheared on transition to a uniform flow. As a result, a homogenisation of the plastics material melt takes place in a simple, efficient and effective manner.


A gearbox assembly for a twin-screw extruder comprises a speed change gearbox for adjusting a screw shaft speed of two screw shafts of the twin-screw extruder, a distribution gearbox allowing the screw shafts to be coupled thereto, and a speed reduction gearbox. The speed change gearbox and the speed reduction gearbox are configured such as to be separable from each other, wherein the speed change gearbox is arranged at a driving end while the speed reduction gearbox couples the speed change gearbox to the distribution gearbox. Due to the fact that the speed change gearbox is configured as an individual gearbox unit arranged at the driving end, an adjustment of the screw shaft speed is easily possible by replacing the speed change gearbox. As a result, a high flexibility and productivity are obtained in the operation of the twin-screw extruder.


A processing installation for the processing of bulk material has a vacuum filter insert for degassing of the bulk material. The vacuum filter insert is arranged in a casing of a screw machine downstream of the feed opening thereof and is provided with at least one filter element so that the vacuum filter insert forms a gas-permeable wall portion which defines the at least one casing bore of the screw machine. Seen in a degassing direction, a protective element comprising a plurality of through-openings is arranged upstream of the at least one filter element. The protective element acts as a granule protection for the at least one filter element and prevents granular bulk material from damaging the at least one filter element. As a result, the vacuum filter insert has a longer service life, thus ensuring a long operating time for the processing installation without interruptions.


A cellular wheel sluice has a housing, a feed shaft opening therein and an outlet shaft opening out therefrom. Arranged between the shafts is a cellular wheel. The latter is arranged so as to be rotatably drivable about a horizontal rotational axis in a cylindrical cellular wheel housing portion. A cellular wheel drive shaft non-rotatably connected to the cellular wheel is rotatably mounted in the housing. A pressure drop is applied during operation of the cellular wheel sluice, a higher pressure being present in the feed shaft than in the outlet shaft. The cellular wheel is operated during the product conveyance between the feed shaft and the outlet shaft at a rotational speed in such a way that an outer periphery of the cellular wheel reaches a speed that is greater than 0.6 m/s.


A processing installation for devolatilization of polymer melts comprises a first extruder and a second extruder arranged downstream thereof in a direction of conveyance. The first extruder comprises several rotatably drivable first shafts which are provided with first treatment members and several devolatilization zones with associated devolatilization ports. Correspondingly, the second extruder comprises several rotatably drivable second shafts which are provided with second treatment members and several second devolatilization zones with associated devolatilization ports. The first treatment members have an external diameter which is smaller than or equal to that of the second treatment members. A devolatilization unit is arranged in a transfer zone which interconnects the extruders. The devolatilization unit comprises a perforated plate and a clearance arranged downstream in the direction of conveyance. A control unit is configured in such a way that when the processing installation is operated, the speed of the second shafts is lower than the speed of the first shafts. The processing installation allows a high devolatilization performance and a high polymer throughput to be achieved at the same time. A throttle is arranged in the transfer zone upstream of the devolatilization unit when seen in the direction of conveyance, with the position of the throttle being adjustable by means of the control unit.

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